DEVELOPMENT OF AN OFF-LINE ENRICHER-REACTOR PROCESS FOR ACTIVATED-SLUDGE DEGRADATION OF HAZARDOUS WASTES

被引:35
作者
BABCOCK, RW [1 ]
RO, KS [1 ]
HSIEH, CC [1 ]
STENSTROM, MK [1 ]
机构
[1] UNIV CALIF LOS ANGELES, DEPT CIVIL ENGN, 4173 ENGN I, LOS ANGELES, CA 90024 USA
关键词
ACTIVATED SLUDGE; BIOAUGMENTATION; BIODEGRADATION; ENRICHER-REACTORS; HAZARDOUS WASTES; 1-NAPHTHYLAMINE;
D O I
10.2175/WER.64.6.5
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The improvement in degradation of a hazardous chemical using a novel bioaugmentation scheme was studied. Bench-scale off-line batch enricher-reactors (ERs) maintaining an enrichment culture were used to bioaugment bench-scale continuous-flow activated sludge reactors treating 1-naphthylamine (1NA). In batch experiments, one-time bioaugmentation inoculations of 1, 2, 5, 10, 20, and 50% by mass of a 1NA-degrading culture (mg mixed liquor volatile suspended solids [MLVSS] of 1NA-degrading culture/mg MLVSS of indigenous culture) increased degradation rates by approximately 0, 33, 100, 100, 100, and 300% respectively over an uninoculated control. In continuous-flow experiments, separate 13.7-L reactors received daily inoculations of 1.4, 2.5,6.6,11.4, and 18.3% by mass of 1NA-degrading culture. Cumulative target compound breakthrough reduction following a 50 mg 1NA/L spike was 13, 21, 11, 35, and 41% compared to an unacclimated control and 4, 13, 1, 27, and 35% compared to an acclimated control, respectively. Similarly, the reduction in breakthrough during reacclimation to 5 mg 1NA/L over six days was 66, 73, 85, 98, and 100%, respectively. A 6% bioaugmented continuous-flow reactor significantly reduced 1NA breakthrough following a step-loading increase from 1 to 5 mg 1NA/L compared to an uninoculated control. Effective bioaugmentation was achieved with additions of biomass equivalent to 14-25% of indigenous cell production rates.
引用
收藏
页码:782 / 791
页数:10
相关论文
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